CN115382413A - Sterile active oxygen water, application thereof in nonreactive cultivation, preparation method and system - Google Patents
Sterile active oxygen water, application thereof in nonreactive cultivation, preparation method and system Download PDFInfo
- Publication number
- CN115382413A CN115382413A CN202211173502.5A CN202211173502A CN115382413A CN 115382413 A CN115382413 A CN 115382413A CN 202211173502 A CN202211173502 A CN 202211173502A CN 115382413 A CN115382413 A CN 115382413A
- Authority
- CN
- China
- Prior art keywords
- water
- active oxygen
- pipe
- pump
- output end
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 252
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 132
- 239000001301 oxygen Substances 0.000 title claims abstract description 132
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 132
- 238000002360 preparation method Methods 0.000 title claims abstract description 26
- 239000007789 gas Substances 0.000 claims abstract description 28
- 235000020188 drinking water Nutrition 0.000 claims abstract description 14
- 239000003651 drinking water Substances 0.000 claims abstract description 14
- 238000009826 distribution Methods 0.000 claims abstract description 8
- 238000002156 mixing Methods 0.000 claims description 15
- 239000003638 chemical reducing agent Substances 0.000 claims description 6
- 239000008213 purified water Substances 0.000 claims description 6
- 238000000746 purification Methods 0.000 claims description 5
- 238000003860 storage Methods 0.000 claims description 5
- -1 polytetrafluoroethylene Polymers 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 238000009423 ventilation Methods 0.000 claims description 3
- 235000020681 well water Nutrition 0.000 claims description 3
- 239000002349 well water Substances 0.000 claims description 3
- 238000001914 filtration Methods 0.000 claims description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 2
- 238000005086 pumping Methods 0.000 claims description 2
- 238000009313 farming Methods 0.000 claims 1
- 150000002926 oxygen Chemical class 0.000 claims 1
- 244000144972 livestock Species 0.000 abstract description 30
- 230000001488 breeding effect Effects 0.000 abstract description 27
- 238000009395 breeding Methods 0.000 abstract description 26
- 239000003242 anti bacterial agent Substances 0.000 description 30
- 229940088710 antibiotic agent Drugs 0.000 description 30
- 241000894006 Bacteria Species 0.000 description 22
- 238000000034 method Methods 0.000 description 17
- 244000144977 poultry Species 0.000 description 15
- 230000001954 sterilising effect Effects 0.000 description 11
- 238000004659 sterilization and disinfection Methods 0.000 description 11
- 206010059866 Drug resistance Diseases 0.000 description 10
- 230000008569 process Effects 0.000 description 9
- 230000008901 benefit Effects 0.000 description 8
- 239000003814 drug Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 8
- 229940079593 drug Drugs 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- 230000001580 bacterial effect Effects 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 6
- 230000009471 action Effects 0.000 description 5
- 230000003115 biocidal effect Effects 0.000 description 5
- 210000004027 cell Anatomy 0.000 description 5
- 235000013305 food Nutrition 0.000 description 5
- 239000002351 wastewater Substances 0.000 description 5
- 102000004190 Enzymes Human genes 0.000 description 4
- 108090000790 Enzymes Proteins 0.000 description 4
- 241000700605 Viruses Species 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 230000006870 function Effects 0.000 description 4
- 235000016709 nutrition Nutrition 0.000 description 4
- 230000035764 nutrition Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 102000014150 Interferons Human genes 0.000 description 3
- 108010050904 Interferons Proteins 0.000 description 3
- 239000004098 Tetracycline Substances 0.000 description 3
- 229940124350 antibacterial drug Drugs 0.000 description 3
- 230000015556 catabolic process Effects 0.000 description 3
- 210000002421 cell wall Anatomy 0.000 description 3
- 238000006731 degradation reaction Methods 0.000 description 3
- 230000002708 enhancing effect Effects 0.000 description 3
- 210000001035 gastrointestinal tract Anatomy 0.000 description 3
- 229940079322 interferon Drugs 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000004060 metabolic process Effects 0.000 description 3
- 230000001590 oxidative effect Effects 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- FDDDEECHVMSUSB-UHFFFAOYSA-N sulfanilamide Chemical compound NC1=CC=C(S(N)(=O)=O)C=C1 FDDDEECHVMSUSB-UHFFFAOYSA-N 0.000 description 3
- 229940124530 sulfonamide Drugs 0.000 description 3
- 239000002352 surface water Substances 0.000 description 3
- 229960002180 tetracycline Drugs 0.000 description 3
- 229930101283 tetracycline Natural products 0.000 description 3
- 235000019364 tetracycline Nutrition 0.000 description 3
- 108091032973 (ribonucleotides)n+m Proteins 0.000 description 2
- KDCGOANMDULRCW-UHFFFAOYSA-N 7H-purine Chemical compound N1=CNC2=NC=NC2=C1 KDCGOANMDULRCW-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 2
- 230000003213 activating effect Effects 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 210000000170 cell membrane Anatomy 0.000 description 2
- 230000034994 death Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 235000013601 eggs Nutrition 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 208000028774 intestinal disease Diseases 0.000 description 2
- 230000007413 intestinal health Effects 0.000 description 2
- 230000002147 killing effect Effects 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 210000004379 membrane Anatomy 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- OFVLGDICTFRJMM-WESIUVDSSA-N tetracycline Chemical compound C1=CC=C2[C@](O)(C)[C@H]3C[C@H]4[C@H](N(C)C)C(O)=C(C(N)=O)C(=O)[C@@]4(O)C(O)=C3C(=O)C2=C1O OFVLGDICTFRJMM-WESIUVDSSA-N 0.000 description 2
- 229940072172 tetracycline antibiotic Drugs 0.000 description 2
- 239000004382 Amylase Substances 0.000 description 1
- 102000013142 Amylases Human genes 0.000 description 1
- 108010065511 Amylases Proteins 0.000 description 1
- 208000035143 Bacterial infection Diseases 0.000 description 1
- 101710132601 Capsid protein Proteins 0.000 description 1
- 101710094648 Coat protein Proteins 0.000 description 1
- 102000004127 Cytokines Human genes 0.000 description 1
- 108090000695 Cytokines Proteins 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 241000287828 Gallus gallus Species 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 102100021181 Golgi phosphoprotein 3 Human genes 0.000 description 1
- 102000015696 Interleukins Human genes 0.000 description 1
- 108010063738 Interleukins Proteins 0.000 description 1
- 102000004895 Lipoproteins Human genes 0.000 description 1
- 108090001030 Lipoproteins Proteins 0.000 description 1
- 101710125418 Major capsid protein Proteins 0.000 description 1
- 206010048723 Multiple-drug resistance Diseases 0.000 description 1
- 101710141454 Nucleoprotein Proteins 0.000 description 1
- 206010034133 Pathogen resistance Diseases 0.000 description 1
- 101710083689 Probable capsid protein Proteins 0.000 description 1
- CZPWVGJYEJSRLH-UHFFFAOYSA-N Pyrimidine Chemical compound C1=CN=CN=C1 CZPWVGJYEJSRLH-UHFFFAOYSA-N 0.000 description 1
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 208000036142 Viral infection Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 235000019418 amylase Nutrition 0.000 description 1
- 239000003674 animal food additive Substances 0.000 description 1
- 208000022362 bacterial infectious disease Diseases 0.000 description 1
- 230000003385 bacteriostatic effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 210000002249 digestive system Anatomy 0.000 description 1
- 230000006806 disease prevention Effects 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000003640 drug residue Substances 0.000 description 1
- 239000002158 endotoxin Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000003031 feeding effect Effects 0.000 description 1
- 238000004401 flow injection analysis Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 210000003714 granulocyte Anatomy 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 230000035876 healing Effects 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 210000002865 immune cell Anatomy 0.000 description 1
- 230000036737 immune function Effects 0.000 description 1
- 230000036039 immunity Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 230000000968 intestinal effect Effects 0.000 description 1
- 210000000265 leukocyte Anatomy 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 229920006008 lipopolysaccharide Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 108020004999 messenger RNA Proteins 0.000 description 1
- 208000030159 metabolic disease Diseases 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 244000000010 microbial pathogen Species 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 210000001616 monocyte Anatomy 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- 230000006855 networking Effects 0.000 description 1
- 231100000957 no side effect Toxicity 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 150000007523 nucleic acids Chemical class 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 210000003463 organelle Anatomy 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000000242 pagocytic effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920001184 polypeptide Polymers 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 235000013406 prebiotics Nutrition 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000003449 preventive effect Effects 0.000 description 1
- 239000006041 probiotic Substances 0.000 description 1
- 235000018291 probiotics Nutrition 0.000 description 1
- 102000004196 processed proteins & peptides Human genes 0.000 description 1
- 108090000765 processed proteins & peptides Proteins 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000010076 replication Effects 0.000 description 1
- 230000008261 resistance mechanism Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 229920002477 rna polymer Polymers 0.000 description 1
- 210000002966 serum Anatomy 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 150000003522 tetracyclines Chemical class 0.000 description 1
- 230000001225 therapeutic effect Effects 0.000 description 1
- 210000001519 tissue Anatomy 0.000 description 1
- 238000013518 transcription Methods 0.000 description 1
- 230000035897 transcription Effects 0.000 description 1
- 238000013519 translation Methods 0.000 description 1
- 230000014616 translation Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
- 230000003612 virological effect Effects 0.000 description 1
- 239000000341 volatile oil Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/70—Pre-treatment of the materials to be mixed
- B01F23/708—Filtering materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/712—Feed mechanisms for feeding fluids
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/305—Treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/38—Organic compounds containing nitrogen
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/40—Organic compounds containing sulfur
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/20—Nature of the water, waste water, sewage or sludge to be treated from animal husbandry
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/02—Specific form of oxidant
- C02F2305/023—Reactive oxygen species, singlet oxygen, OH radical
Abstract
The invention relates to the technical field of livestock breeding drinking water treatment equipment, and particularly discloses sterile active oxygen water and an application and a preparation method and a system thereof in nonreactive breeding, wherein the input end of a pipeline pump is connected with a raw water tank, the output end of the pipeline pump is connected with a filter, a cluster jet mixer consists of an outlet water flow combining pipe, an inlet water distribution pipe connected with the output end of the filter, a gas distribution pipe connected with the output end of active oxygen generation equipment, a plurality of small-hole jet devices of which the water inlet ends are connected with the inlet water distribution pipe and the water outlet ends are connected with the outlet water flow combining pipe, and a plurality of gas pipes of which the two ends are respectively connected with the inlet end and the gas distribution pipe of the small-hole jet devices, a water purifying tank is connected with the outlet water flow combining pipe, the input end and the outlet end of a water supply pump are respectively connected with a water purifying tank and a water supply pipeline, a tank type equipment room is used for accommodating the active oxygen water preparation equipment, and the active oxygen concentration of the active oxygen water in the water supply pipeline is 0.5-1.2 ppm, so that the nonreactive breeding pasture can provide healthy drinking water for livestock efficiently, with low cost and without pollution.
Description
Technical Field
The invention relates to the technical field of livestock breeding drinking water treatment equipment, in particular to a sterile active oxygen water preparation system based on antibiotic-free breeding.
Background
At present, livestock and poultry breeding forms specialization, intensification and scale in China, and the living requirements of people are greatly met. Meanwhile, the intensive and large-scale cultivation increases the cultivation difficulty, and the traditional antibiotics are used in biological prevention and control and disease prevention, so that the serious consequences are brought to the food safety and the environmental pollution. With the increasing requirements of the state on food safety, the livestock and poultry breeding industry changes from a conventional breeding mode taking yield as a target to a resistance-reducing or non-resistance breeding mode with high quality and high efficiency. Only by continuously seeking new technology and new modes, the breeding enterprises can continuously develop and strengthen the breeding effect of reducing resistance and no resistance and improve the breeding quality and benefit, and good economic benefit and social benefit are obtained.
At present, all countries of breeding enterprises are actively researching antibiotic reducing and replacing products or schemes, and besides the breeding enterprises, feed companies are also searching for substitutes of antibiotics. But clearly no single solution has been found that can replace antibiotics. Researchers have conducted a number of trials over the last 20 years to find alternatives to antibiotics, these studies being mainly conducted in europe (sweden, denmark, the netherlands) where antibiotics were first banned and strictly regulated by regulations. These studies have found a series of antibiotic alternatives with antibacterial effects.
At present, a plurality of antibiotic substitutes are commonly used in the livestock breeding industry, such as probiotics, prebiotics, enzymes, plant antibiotics, minerals, essential oil or polysaccharide. However, the few-antibody and alternative-antibody schemes start from feed addition, and aim at intestinal health of livestock. The supply of safe drinking water and the prevention of animal intestinal diseases are inevitable processes in the breeding process.
At present, the water for cultivation is generally common water, and has the following modes and characteristics:
1. underground water (surface water) is directly drunk by livestock after being precipitated or micro-filtered, the water treatment mode does not improve the water quality, and although the water treatment mode has the advantages of no wastewater and low cost, no sterilization process is adopted, and the potential biological safety hazard is caused.
2. The method is characterized in that chemical disinfector is added after underground water (surface water) is precipitated or micro-filtered and then is drunk by livestock, microorganisms in the water are treated by the water treatment mode, although the method has the advantages of simple process, no wastewater and low cost, the drug adding amount is difficult to control accurately, the mixed sterilization effect cannot be guaranteed, chemical drug residues exist, and drinking water is influenced.
3. Underground water (surface water) is subjected to precipitation or microfiltration and then subjected to ultrafiltration and reverse osmosis treatment and then is drunk by livestock, and the water treatment mode of the treatment enables the water quality to be pure and is suitable for purification of various types of raw water, but the material investment and the operation cost are high, and a large amount of wastewater is discharged.
The water supply modes have the problems of potential biological safety hazards of the drinking water system, generation of a large amount of wastewater pollutants or high investment cost and the like in different degrees. Especially, under the condition of water source environmental pollution, the intensive and large-scale breeding mode has direct influence on breeding indexes such as the survival rate of livestock, the feed-meat ratio, the medicine ratio and the like.
Therefore, there is a need in the livestock breeding industry to provide drinking water with bactericidal and bacteriostatic effects, no residue and no drug resistance, so as to improve the intestinal micro-ecological environment of livestock, promote intestinal health and reduce or eliminate the use of antibiotics.
Disclosure of Invention
Aiming at solving the problem that the nonreactive breeding pasture in the prior art is difficult to provide healthy drinking water for livestock in an efficient, low-cost and pollution-free manner, the invention designs the sterile active oxygen water and the application and preparation method and system thereof in nonreactive breeding.
In order to achieve the purpose, the invention provides the following technical scheme: the sterile active oxygen water preparation system comprises a raw water tank, a water lifting pump for supplying underground well water into the raw water tank and a water supply pipeline connected with the output end of the raw water tank, wherein the input end of the pipeline pump is connected with the output end of the raw water tank; the input end of the filter is connected with the output end of the pipeline pump; the active oxygen generating equipment is controlled by frequency conversion, and the concentration of active oxygen prepared by the active oxygen generating equipment is adjustable within the range of 20-100%; the cluster jet mixer consists of an outlet water merging pipe, an inlet water dividing pipe with an input end connected with the output end of the filter, a gas dividing pipe with an input end connected with the output end of the active oxygen generating equipment, a plurality of small-hole jet devices with water inlet ends connected with branch pipe joints of the inlet water dividing pipe and water outlet ends connected with branch pipe joints of the outlet water merging pipe, and a plurality of gas pipes with two ends respectively connected with the gas inlet end of each small-hole jet device and the branch pipe joints of the gas dividing pipe; the input end of the water purifying tank is connected with the output end of the water outlet flow merging pipe; the input end of the water supply pump is connected with the output end of the purified water tank, and the output end of the water supply pump is connected with a water supply pipeline; the box type equipment room is used for accommodating the pipeline pump, the filter, the active oxygen generating equipment, the cluster type jet flow mixer, the purified water tank and the water supply pump; the concentration of the residual active oxygen in the active oxygen water at the output end of the water outlet flow combining pipe is 2-4 ppm.
Preferably, the aperture ejector is corresponding to intake end, play water end and inlet end department and is intake interface, play water interface and the interface that admits air respectively, intake interface with be equipped with the connection pipeline section along the axial in proper order between the play water interface, reduce the pipeline section, mix pipeline section and diffusion pipeline section, the interface that admits air is along the perpendicular to the direction of intake interface and play water interface axis with mix the pipeline section and be connected.
Preferably, the length of the diffuser section is greater than the length of the reducer section, and the length of the reducer section is greater than the length of the mixing section.
Preferably, the box-type equipment room is a container-type heat preservation room, a temperature control device and a ventilation facility are arranged in the box-type equipment room, and the pipeline pump, the filter, the active oxygen generating device, the cluster jet mixer, the water purification tank and the water supply pump are fixedly arranged on the bottom plate of the inner cavity of the box-type equipment room respectively.
Preferably, the filter is a nano-scale filter.
Preferably, the water supply pump is a stainless steel constant pressure water pump.
Preferably, the gas pipe is a polytetrafluoroethylene pipe.
The preparation method of the sterile active oxygen water comprises the following steps:
s1, pumping underground water from a water well by using a water pump, and injecting the underground water into a raw water tank for storage;
s2, extracting the stored raw water from the raw water tank by using a pipeline pump, and injecting the extracted raw water into a filter for filtering;
s3, inputting the filtered raw water into a water inlet shunt pipe, enabling the raw water in the water inlet shunt pipe to flow into a small-hole ejector through a branch pipe joint respectively, inputting active oxygen generated by active oxygen generating equipment into a gas branch pipe, inputting the active oxygen in the gas branch pipe from the gas inlet end of the small-hole ejector through a branch pipe connector and the gas pipe in sequence, and efficiently and fully mixing the active oxygen and the raw water in the inner cavity of the small-hole ejector to prepare primary active oxygen water with the residual active oxygen concentration of 2-4 ppm;
s4, inputting the primary active oxygen water into a purified water tank for storage;
and S5, the active oxygen water which is pumped from the water purifying tank by the water supply pump and is conveyed to the water supply pipeline is the sterile active oxygen water.
The concentration of the sterile active oxygen water as drinking water is 0.5-1.2 ppm.
Preferably, the sterile active oxygen water is applied to nonreactive culture.
Wherein, the main mechanism of active oxygen sterilization is as follows:
the active oxygen is a strong oxidant, the molecules of the active oxygen are extremely unstable, the active oxygen can be decomposed to generate monatomic oxygen (O) and hydroxyl (OH) with extremely strong oxidizing power, the active oxygen is a unique bacteria-melting preparation, the active oxygen can be quickly melted into cell walls, the internal structures of microorganisms such as bacteria, viruses and the like can be damaged, and the active oxygen has extremely strong killing effect on various pathogenic microorganisms.
The sterilization process of active oxygen belongs to biochemical oxidation reaction. The function is mainly realized by the following forms: 1) The active oxygen can oxidize and decompose enzyme required by glucose in the bacteria to inactivate and kill the bacteria; 2) Acts on nuclear substances in bacterial cells, such as purine and pyrimidine in nucleic acid, destroys organelle, DNA and RNA, and destroys metabolism of bacteria, resulting in bacterial death; 3) The active oxygen reacts with lipid double chains of bacterial cell walls, penetrates cell membrane tissues, invades cells, and acts on lipoprotein of an outer membrane and lipopolysaccharide inside the outer membrane to enable bacteria to be dissolved and killed due to permeability distortion and metabolism disorder; 4) The live oxygen acts on 4 polypeptide chains of coat protein of virus to damage RNA and DNA, and destroys protein forming it, thereby resulting in virus death. After oxidation of the phage by live oxygen, the coat is broken into many fragments, from which many ribonucleic acids are released, interfering with their ability to adsorb to the registers.
In addition, the active oxygen can stimulate the proliferation of leukocytes of the body, enhance the phagocytic function of granulocytes and further stimulate the formation of monocytes, which all contribute to the killing of bacteria, fungi and viruses.
The active oxygen can also react with unsaturated fatty acid on the surface of immune cells to generate a lipid hydrogen peroxide chain, and the lipid hydrogen peroxide chain enters the cells and can activate nuclear factor NFKD, thereby activating the replication, transcription and translation of cell MRNA, promoting the synthesis of protein, releasing cytokines (interferon and interleukin) and enhancing the immune function of organisms. Clinical studies confirmed that: when the therapeutic concentration of active oxygen reaches 50ug/ml, the interferon in the serum reaches a maximum value, and the interferon can accelerate the healing of viral and bacterial infections.
The effect of the active oxygen water with proper concentration on the digestive system of livestock and poultry:
the active oxygen is made into active oxygen water with proper concentration for livestock and poultry to drink, and the sterile active oxygen water has the functions of sterilization and bacteriostasis and can adjust the micro-ecological environment of the intestinal tracts of the livestock and poultry. The live oxygen reduces the number of bacteria living in host nutrition in intestinal tracts of livestock and poultry, and reduces the consumption of the host nutrition. Meanwhile, the active oxygen decomposition product is oxygen, so that the biological feed additive is non-toxic, free of side effects, free of residues and pollution, and capable of activating cells, enhancing metabolism, improving immunity, enhancing activity of secreted amylase, improving utilization rate of food nutrition components of livestock and poultry, especially young livestock and poultry, increasing nutrition supply of young livestock and poultry, and promoting healthy growth of livestock and poultry.
The significance of decomposing and replacing antibiotics in the livestock and poultry breeding process is as follows:
the active oxygen sterilization capacity is 600 times of that of antibiotics, and the alcohol sterilization capacity is 1000 times of that of alcohol, so that the active oxygen sterilization agent is a good substitute for the antibiotics, and has no side effect, drug resistance and residue. At present, the abuse of antibiotics, meat, egg and milk antibiotic residues, super drug-resistant bacteria and the like are important problems influencing the development of livestock and poultry breeding industry, and the active oxygen not only has the capacity of decomposing chemical drugs (antibiotics) but also can replace the antibiotics, thereby fundamentally ensuring the breeding and food safety.
Effect of live oxygen on antibiotics:
the degradation efficiency of the strong oxidation of the active oxygen to the tetracycline antibiotics (TCs) is very high, the tetracycline (TET) can be completely removed only by the active oxygen treatment for 4-6 min, for example, the TET with the concentration of 20mg/L can be completely degraded by the active oxygen treatment for 5 min.
8 kinds of sulfanilamide antibiotics in the water solution are degraded by adopting an active oxygen oxidation method, the degradation influence of active oxygen action time on the 8 kinds of sulfanilamide antibiotics is analyzed, and the reaction kinetics of removing the antibiotics in the water by the active oxygen oxidation is advancedA study was conducted. The results show that the active oxygen oxidation method can completely remove SIZ, SN, SCPD, SDZ and SMX, and the removal rates of SMR, SG and SA are respectively 99.30%, 98.19% and 98.49%. The degradation of 8 kinds of sulfanilamide antibiotics by the active oxygen oxidation method accords with first-order reaction kinetics, and the reaction rate constant is 0.0547-0.1210 min -1 。
Effect of live oxygen on superbacteria:
the term "multi-drug resistant bacterium" refers to a bacterium that is not resistant to a single species of bacteria, but rather to a plurality of antibiotics. Such bacteria have a strong resistance to antibiotics and can evade the danger of being killed. Genetic mutations are the underlying cause of the production of superbacteria. The development of bacterial resistance is a consequence of the widespread clinical use of antibiotics, and the abuse of antibiotics accelerates this process. The abuse of antibiotics destroys the contradiction between the antibacterial drugs and the drug resistance of bacteria in a balanced state, the bacteria with drug resistance capability also obtain the drug resistance capability aiming at different antibacterial drugs through continuous evolution and variation, the capability is continuously strengthened in the contradiction conflict, and the bacteria gradually become drug-resistant super bacteria from single drug resistance to multiple drug resistance and even universal drug resistance. The drug resistance mechanism mainly comprises: 1) Bacteria produce inactivated enzyme or inactivated enzyme, and destroy the structure of antibiotics to make them inactive; 2) The structure and the quantity of target proteins acting as antibiotics are changed, so that bacteria are not sensitive to the antibiotics any more; 3) The permeability of the bacterial cell membrane is changed, so that antibiotics can not enter the interior of the thallus; 4) The bacteria actively expel the antibiotics out of the bacteria under the action of a drug efflux pump; 5) The formation of bacterial biofilm reduces antibiotic action. The active oxygen has single structure and strong oxidizing power, can be quickly fused into bacterial cell walls to destroy the internal structure of the bacteria, cannot generate the situation of drug resistance, and fundamentally solves the formation of the super bacteria.
Compared with the prior art, the invention has the beneficial effects that:
1. the sterile active oxygen water preparation system is disposable input equipment, can be benefited for a long time, has no material consumption and no waste water in the active oxygen water preparation process, and accords with the national policy of energy conservation and water conservation.
2. The sterile active oxygen water preparation system can be used for preparing sterile active oxygen water immediately, biological safety and constant-pressure healthy drinking water of the whole drinking water system of a pasture are guaranteed, intestinal diseases of livestock and poultry caused by the drinking water system are avoided, and preventive antibacterial drugs are put in the drinking water system.
3. In the active oxygen water prepared by the sterile active oxygen water preparation system, the active oxygen has super-strong sterilization capability, no residue and no drug resistance, is superior to the feeding effect of various antibiotics, greatly improves the content of egg quality in livestock meat, saves a large amount of manpower and material resources for feeding the drugs, is an ideal mode of antibiotic-free breeding, and is an effective measure for food safety guarantee.
4. The active oxygen water prepared by the sterile active oxygen water preparation system has the functions of sterilization and bacteriostasis, is beneficial to adjusting the micro-ecological environment of animal intestinal tracts, strengthens the metabolism, improves the absorption rate of livestock to nutrient components, reduces the feed conversion ratio and reduces the feed cost. The economic benefit is obvious, and the method has great social benefit in the aspect of grain safety.
5. The use of the sterile active oxygen water preparation system can greatly reduce the use of antibiotics, makes important contribution to environmental protection, and has great social benefit.
Drawings
FIG. 1 is a schematic diagram of the system of the present invention;
fig. 2 is a schematic sectional structure diagram of the orifice ejector of the present invention.
In the figure: 1-raw water tank; 2-a water lifting pump; 3-a pipeline pump; 4-a filter; 5-a live oxygen generating device; 6-a cluster jet mixer; 61-water inlet and water distribution pipe; 62-a gas distribution pipe; 63-outlet water mixing pipe; 64-orifice jet device; 641-water inlet interface; 642-water outlet interface; 643 — an air intake interface; 644-connecting pipe section; 645-reduction of the tube section; 646-a diffuser section; 647-mixing section; 65-trachea; 7-a water purifying tank; 8-water supply pump; 9-box type equipment room.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-2, the antibiotic-free culture-based sterile active oxygen water preparation system comprises a raw water tank 1, a water lifting pump 2 for supplying underground well water into the raw water tank 1, and a water supply pipeline connected with the output end of the raw water tank 1, wherein the input end of a pipeline pump 3 is connected with the output end of the raw water tank 1; the input end of the filter 4 is connected with the output end of the pipeline pump 3; the active oxygen generating equipment 5 adopts frequency conversion control, and the concentration of the prepared active oxygen is adjustable within the range of 20-100%; the cluster jet mixer 6 consists of an outlet water merging pipe 63, an inlet water dividing pipe 61 with the input end connected with the output end of the filter 4, a gas distributing pipe 62 with the input end connected with the output end of the active oxygen generating equipment 5, a plurality of small-hole jet devices 64 with the water inlet ends connected with the branch pipe joints of the inlet water dividing pipe 61 and the water outlet ends connected with the branch pipe joints of the outlet water merging pipe 63, and a plurality of gas pipes 65 with the two ends respectively connected with the gas inlet ends of the small-hole jet devices 64 and the branch pipe joints of the gas distributing pipe 62; the input end of the water purifying tank 7 is connected with the output end of the water outlet confluence pipe 63; the input end of the water supply pump 8 is connected with the output end of the purified water tank 7, and the output end of the water supply pump 8 is connected with a water supply pipeline; the box type equipment room 9 is used for accommodating the pipeline pump 3, the filter 4, the active oxygen generating equipment 5, the cluster type jet mixer 6, the purified water tank 7 and the water supply pump 8; the concentration of the residual active oxygen in the active oxygen water at the output end of the water outlet confluence pipe 63 is 2-4 ppm.
In conclusion, the water lifting pump 2 pumps the underground water from the well and injects the underground water into the raw water tank 1 for storage; the pipeline pump 3 pumps and stores raw water from the raw water tank 1 and injects the raw water into the active oxygen water preparation system; raw water enters the water inlet diversion pipe 61 after being filtered by the filter 4, and the raw water in the water inlet diversion pipe 61 respectively flows into the small-hole jet device 64 through the branch pipe joint; the active oxygen generated by the active oxygen generating equipment 5 is input into the air distributing pipe 62, the active oxygen in the air distributing pipe 62 is respectively input from the air inlet end of the small hole ejector 64 through the branch pipe interface and the air pipe 65, the active oxygen and the raw water are efficiently and fully mixed in the inner cavity of the small hole ejector 64 to prepare active oxygen water with the residual active oxygen concentration of 2-4 ppm, and the active oxygen water is cached in the water purifying tank 7 and then input into a water supply pipeline through the water supply pump 8 for poultry and livestock to drink.
Wherein, under the standard atmospheric pressure, 1 volume of water dissolves 0.494 volume of active oxygen, and both temperature and pressure are factors influencing the solubility of the active oxygen in the water. The higher the mixing efficiency is, the higher the solubility of the active oxygen is on the premise that the treated water quantity, the water temperature and the active oxygen concentration are the same; the contact area of the active oxygen and the water is large under certain pressure (that is, the flow and the pressure of the water flow injection and the added active oxygen amount reach the proper proportion, the more and more uniform the formed micro-bubbles), the mixing efficiency is high, and the small-hole jet device 64 is an ideal mixing device and is simple and reliable to install. The water flow with a certain pressure enters each small-hole ejector 64, and the active oxygen and the water flow out after being efficiently mixed and dissolved. According to various water purification requirements, the corresponding number of jet device units are configured, various water quantity requirements can be met, and because the water flow passes through the small-hole jet device 64 with the best mixing and dissolving effects, the active oxygen content of the active oxygen water flowing out of the water outlet flow combiner is uniform, and the sterilization effect is stable.
The live oxygen generator combination with corresponding specification, the jet mixer combination with corresponding specification and the reasonable water pump pipeline valve specification can be configured according to the breeding scale and the breeding category so as to meet the drinking requirements of livestock with different water qualities, different live oxygen concentrations and water yields.
The half-life period of the active oxygen in the water is only 20-30 min, so that the residual active oxygen concentration in the prepared active oxygen water reaches 2-4 ppm, and the high-quality active oxygen water (the active oxygen concentration is 0.5-1.2 ppm) with a certain concentration can be guaranteed to be drunk by livestock and poultry.
In addition, above-mentioned active oxygen water preparation system can dispose intelligent thing networking module, realizes central centralized control, data acquisition uploads, cell-phone APP software control etc. but remote monitoring equipment operation conditions and quality of water, water yield situation realize unmanned on duty.
The box type equipment room 9 is simple and quick to install and can be placed only by a hardening plane with a corresponding area.
In this embodiment, the small hole jet device 64 is provided with a water inlet interface 641, a water outlet interface 642 and a gas inlet interface 643 corresponding to the water inlet end, the water outlet end and the gas inlet end, respectively, a connecting pipe segment 644, a reducing pipe segment 645, a mixing pipe segment 647 and a diffusing pipe segment 646 are sequentially arranged between the water inlet interface 641 and the water outlet interface 642 along the axial direction, and the gas inlet interface 643 is connected with the mixing pipe segment 647 along the direction perpendicular to the axial direction of the water inlet interface 641 and the water outlet interface 642.
In this embodiment, the length of the diffuser section 646 is greater than the length of the reducer section 645, and the length of the reducer section 645 is greater than the length of the mixing section 647.
In this embodiment, the box-type equipment room 9 is a container-type heat preservation room, a temperature control device and a ventilation facility are provided in the box-type equipment room 9, and the pipe pump 3, the filter 4, the active oxygen generating device 5, the cluster-type jet mixer 6, the water purification tank 7 and the water supply pump 8 are respectively fixedly installed on the bottom plate of the inner cavity of the box-type equipment room 9.
In this embodiment, the filter 4 is a nano-scale filter.
In this embodiment, the water supply pump 8 is a stainless steel constant pressure water pump.
In this embodiment, the air tube 65 is a teflon tube.
The experimental data of the effect verification of the sterile active oxygen water in the chicken farm are as follows:
it is noted that, herein, relational terms such as first and second, and the like may be used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that various changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (10)
1. Aseptic active oxygen water preparation system, including former water tank (1), be used for infeeding underground well water lift pump (2) in former water tank (1) and with the water supply pipeline that former water tank (1) output is connected, its characterized in that still includes:
the input end of the pipeline pump (3) is connected with the output end of the raw water tank (1);
the input end of the filter (4) is connected with the output end of the pipeline pump (3);
the active oxygen generating equipment (5) adopts variable frequency control, and the concentration of the prepared active oxygen is adjustable within the range of 20-100%;
the cluster jet mixer (6) consists of a water outlet confluence pipe (63), a water inlet shunt pipe (61) with an input end connected with the output end of the filter (4), a gas distribution pipe (62) with an input end connected with the output end of the active oxygen generating equipment (5), a plurality of small-hole jet devices (64) with water inlet ends connected with branch pipe joints of the water inlet shunt pipe (61) and water outlet ends connected with branch pipe joints of the water outlet confluence pipe (63), and a plurality of gas pipes (65) with two ends respectively connected with the gas inlet ends of the small-hole jet devices (64) and the branch pipe joints of the gas distribution pipe (62);
the input end of the water purifying tank (7) is connected with the output end of the effluent flow combining pipe (63);
the input end of the water supply pump (8) is connected with the output end of the purified water tank (7), and the output end of the water supply pump (8) is connected with a water supply pipeline; and
a box-type equipment room (9), wherein the box-type equipment room (9) is used for accommodating the pipeline pump (3), the filter (4), the active oxygen generating equipment (5), the cluster jet mixer (6), the water purifying tank (7) and the water supply pump (8);
the concentration of the residual active oxygen in the active oxygen water at the output end of the water outlet confluence pipe (63) is 2-4 ppm.
2. The sterile activated water preparation system according to claim 1, wherein: the small-hole ejector (64) is provided with a water inlet interface (641), a water outlet interface (642) and an air inlet interface (643) corresponding to the water inlet end, the water outlet end and the air inlet end respectively, a connecting pipe section (644), a reducing pipe section (645), a mixing pipe section (647) and a diffusing pipe section (646) are sequentially arranged between the water inlet interface (641) and the water outlet interface (642) along the axial direction, and the air inlet interface (643) is connected with the mixing pipe section (647) along the direction perpendicular to the axial lines of the water inlet interface (641) and the water outlet interface (642).
3. The aseptic activated oxygen water preparation system according to claim 2, wherein: the length of the diffuser section (646) is greater than the length of the reducer section (645), and the length of the reducer section (645) is greater than the length of the mixing section (647).
4. The sterile activated water preparation system according to claim 1, wherein: box equipment room (9) are container formula insulated building, be equipped with temperature control equipment and ventilation facilities in box equipment room (9), tubing pump (3), filter (4), active oxygen generating equipment (5), cluster type jet mixer (6), water purification case (7) and working pump (8) fixed mounting respectively in on the bottom plate of box equipment room (9) inner chamber.
5. The sterile activated water preparation system according to claim 1, wherein: the filter (4) is a nano-scale filter.
6. The sterile activated water preparation system according to claim 1, wherein: the water supply pump (8) is a stainless steel constant-pressure water pump.
7. The sterile activated water preparation system according to claim 1, wherein: the air pipe (65) is a polytetrafluoroethylene pipe.
8. The preparation method of the sterile active oxygen water is characterized by comprising the following steps:
s1, pumping underground water from a well by using a water pump (2) and injecting the underground water into a raw water tank (1) for storage;
s2, extracting stored raw water from the raw water tank (1) by using a pipeline pump (3), and injecting the extracted raw water into a filter (4) for filtering;
s3, inputting the filtered raw water into a water inlet shunt pipe (61), enabling the raw water in the water inlet shunt pipe (61) to flow into a small-hole ejector (64) through a branch pipe joint respectively, inputting active oxygen generated by active oxygen generating equipment (5) into a gas shunt pipe (62), enabling the active oxygen in the gas shunt pipe (62) to be sequentially input from the gas inlet end of the small-hole ejector (64) through a branch pipe joint and a gas pipe (65) respectively, and efficiently and fully mixing the active oxygen and the raw water in the inner cavity of the small-hole ejector (64) to prepare primary active oxygen water with the residual active oxygen concentration of 2-4 ppm;
s4, inputting the primary active oxygen water into a water purifying tank (7) for storage;
and S5, the active oxygen water which is extracted from the water purifying tank (7) by the water supply pump (8) and is conveyed to the water supply pipeline is the sterile active oxygen water.
9. Sterile active oxygen water, its characterized in that: the concentration of the sterile active oxygen water as drinking water is 0.5-1.2 ppm.
10. The use of sterile and oxygenated water according to claim 9 in nonreactive farming.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211173502.5A CN115382413A (en) | 2022-09-26 | 2022-09-26 | Sterile active oxygen water, application thereof in nonreactive cultivation, preparation method and system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211173502.5A CN115382413A (en) | 2022-09-26 | 2022-09-26 | Sterile active oxygen water, application thereof in nonreactive cultivation, preparation method and system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN115382413A true CN115382413A (en) | 2022-11-25 |
Family
ID=84127893
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202211173502.5A Pending CN115382413A (en) | 2022-09-26 | 2022-09-26 | Sterile active oxygen water, application thereof in nonreactive cultivation, preparation method and system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN115382413A (en) |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1912728A1 (en) * | 2005-08-02 | 2008-04-23 | JohnsonDiversey, Inc. | Mixing eductor |
| KR20080105008A (en) * | 2008-07-02 | 2008-12-03 | (주)지앤지코리아 | Apparatus and method for generating micro bubbles |
| CN102764605A (en) * | 2012-07-30 | 2012-11-07 | 西藏创源水资源科技有限责任公司 | Method and device producing high-oxygen water without electricity |
| CN202785825U (en) * | 2012-07-23 | 2013-03-13 | 北京中农天陆微纳米气泡水科技有限公司 | Sterilization and oxygen enrichment equipment for aquaculture |
| CN107115798A (en) * | 2017-04-24 | 2017-09-01 | 杭州天霁环境科技有限公司 | High-oxygen water preparation system |
| CN207201766U (en) * | 2016-12-15 | 2018-04-10 | 广东海威水产养殖有限公司 | A kind of racetrack circulating water cultivation oxygen-enriching system |
| CN209442795U (en) * | 2019-01-30 | 2019-09-27 | 四川亿海环保工程有限公司 | A kind of drinking water purification system |
| CN112439330A (en) * | 2019-08-30 | 2021-03-05 | 宁波方太厨具有限公司 | Micro-nano bubble generating device and cleaning machine applying same |
| CN114931870A (en) * | 2022-05-31 | 2022-08-23 | 佛山市美的清湖净水设备有限公司 | Water purifier and water outlet control system and method thereof |
-
2022
- 2022-09-26 CN CN202211173502.5A patent/CN115382413A/en active Pending
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1912728A1 (en) * | 2005-08-02 | 2008-04-23 | JohnsonDiversey, Inc. | Mixing eductor |
| KR20080105008A (en) * | 2008-07-02 | 2008-12-03 | (주)지앤지코리아 | Apparatus and method for generating micro bubbles |
| CN202785825U (en) * | 2012-07-23 | 2013-03-13 | 北京中农天陆微纳米气泡水科技有限公司 | Sterilization and oxygen enrichment equipment for aquaculture |
| CN102764605A (en) * | 2012-07-30 | 2012-11-07 | 西藏创源水资源科技有限责任公司 | Method and device producing high-oxygen water without electricity |
| CN207201766U (en) * | 2016-12-15 | 2018-04-10 | 广东海威水产养殖有限公司 | A kind of racetrack circulating water cultivation oxygen-enriching system |
| CN107115798A (en) * | 2017-04-24 | 2017-09-01 | 杭州天霁环境科技有限公司 | High-oxygen water preparation system |
| CN209442795U (en) * | 2019-01-30 | 2019-09-27 | 四川亿海环保工程有限公司 | A kind of drinking water purification system |
| CN112439330A (en) * | 2019-08-30 | 2021-03-05 | 宁波方太厨具有限公司 | Micro-nano bubble generating device and cleaning machine applying same |
| CN114931870A (en) * | 2022-05-31 | 2022-08-23 | 佛山市美的清湖净水设备有限公司 | Water purifier and water outlet control system and method thereof |
Non-Patent Citations (1)
| Title |
|---|
| 北京市环境保护科学研究所编: "水污染防治手册", vol. 1, 上海科学技术出版社, pages: 463 * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101475288A (en) | Water circulation filtering system for aquiculture | |
| CN101897315A (en) | Live stock feeding method | |
| CN110790362B (en) | Method for simultaneously removing antibiotics and heavy metals in livestock and poultry breeding wastewater | |
| CN103693802A (en) | Treating method for wastewater from vitamin B2 production | |
| CN2895396Y (en) | Nano titanium dioxide dicinfecting and water treatment apparatus | |
| CN115382413A (en) | Sterile active oxygen water, application thereof in nonreactive cultivation, preparation method and system | |
| CN103695352A (en) | Method for manufacturing water-quality treating agent specific to waste water of Chinese date processing plant by adopting microbial fermentation process | |
| CN202519077U (en) | High-efficiency water-drinking environment-friendly disinfection device for poultries and livestock | |
| Huang et al. | Removal of antibiotic resistance genes during livestock wastewater treatment processes: Review and prospects | |
| CN107047438A (en) | A kind of purification reduction apparatus of water used for aquiculture | |
| CN103444618B (en) | A kind ofly remove suspended particulate, the ozone adding set of degradation of organic substances and method thereof | |
| CN113754203B (en) | Treatment method of aquaculture tail water | |
| CN202514432U (en) | Environment-friendly disinfection aerator | |
| CN104671587A (en) | Cycling treatment device for water of fish tank | |
| CN110856480A (en) | Intelligent aquatic product culture system | |
| CN210394127U (en) | Sewage treatment device for dairy farm | |
| CN210642011U (en) | Circulating seawater culture system based on microalgae-strain bioreactor | |
| CN111718055A (en) | High-oxidation treatment process for purifying temporary culture water of fresh fish | |
| CN205756579U (en) | Efficient circulation water cultivating system | |
| CN113508773A (en) | Shellfish circulating water temporary culture system and shellfish heavy metal purification method | |
| CN102942244B (en) | High-density aquaculture oxygenation purification method and system | |
| CN214218447U (en) | Sewage treatment device for farm | |
| CN213246445U (en) | Portable multifunctional combined fish culture device in tung cell chamber | |
| CN104609644B (en) | Aquaculture methane-generating pit goes out method for treating water | |
| CN217230959U (en) | Machine is made to hypochlorous acid water antiseptic solution |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |